Similar to Example 4.5-2 in F&R, 3rd Ed. One of our clients has asked our Bison Engineering and Evaluation Firm (BEEF, Inc.) to evaluate a multi-unit chemical process that recovers solid potassium chromate salt from an aqueous solution. The client has provide a description of the chemical process, as given in the next paragraph. A feed stream of potassium chromate solution is sent to an evaporator where heat boils off some water as steam and produces a concentrated solution containing 49.4 wt% K2CrO4. This concentrated stream is fed into a crystallizer in which the solution is cooled causing potassium chromate crystals to form, and then the solution with suspended crystals is filtered. The filter cake contains solid crystals with an entrapped solution of 36.36 wt% dissolved K2CrO4. The crystals account for 95% of the total mass of the filter cake. The solution that passes through the filter is recycled back to the beginning of the multi-unit process. This recycle stream containing 36.36 wt% K2CrO4 is mixed with 4.500 x 103 kg/h of a fresh aqueous solution to the multi-unit process that contains one-third potassium chromate by mass. The resulting stream from the mixing is then fed into the evaporator. Your project supervisor has asked you to complete the material balances on this multi-unit process. You are to determine the flow rate of the steam leaving the evaporator, the rate of production of crystalline K2CrO4, the feed rates that the evaporator and crystallizer must be designed to handle, and the ratio (kg recycle per kg fresh feed). Also, what is the composition of the feed to the evaporator? 1/3 2/3 v90.10.04 © 2007, Michael E. Hanyak, Jr., All Rights Reserved Page 5-40 1/3 2/3 v90.10.04 © 2007, Michael E. Hanyak, Jr., All Rights Reserved Page 5-41 1/3 Click here to view the Excel "EZ Setup"/ Solver file containing solutions of several mathematical models and a mathematical algorithm. This file also demonstrates the financial benefit of recycling materials. v90.10.04 © 2007, Michael E. Hanyak, Jr., All Rights Reserved Page 5-42 1/3 2/3 v90.10.04 © 2007, Michael E. Hanyak, Jr., All Rights Reserved Page 5-43
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